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Improved ethylene polymerization catalyst composition

A technology of ethylene copolymers and compositions, applied in the field of Ziegler-Natta catalyst compositions, which can solve the problems of decreased melt flow rate, decreased introduction of comonomers, uneven polymers, etc.

Inactive Publication Date: 2012-03-21
BOREALIS AG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0020] For example, this catalyst composition shows a change in comonomer response over time, resulting in a significant decrease in comonomer incorporation during the first phase of polymerization.
This further leads to an increase in density during the copolymerization
[0021] A further disadvantage is that the use of usual Ziegler-Natta catalyst compositions often leads to a significant decrease in the melt flow rate (MRF) and a respective increase in the molecular weight during the first phase of the copolymerization
[0022] If the polymerization process is a continuous multistage process, this so-called "time drift" in catalyst performance can cause further problems, where the residence time distribution combined with the "time drift" problem can lead to inhomogeneity of the polymer produced

Method used

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  • Improved ethylene polymerization catalyst composition
  • Improved ethylene polymerization catalyst composition

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Experimental program
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Effect test

Embodiment

[0157] 1. Catalyst Preparation

[0158] a) Preparation of Mg complex

[0159] 87 kg of toluene were charged to the multipurpose reactor. Then 45.5 kg of Bomag A (20% in heptane) were added to the reactor. 2-Ethyl-1-hexanol (2-EHA) was then added to the reactor at a flow rate of 24-40 kg / h. 2-EHA has been dried over molecular sieves. Keep the reaction temperature below 38°C. The solution was mixed for 30 minutes and cooled to room temperature.

[0160] The molar ratio of BOMAG-A to 2-ethyl-1-hexanol was 1:1.83.

[0161] b) Preparation of solid catalyst component:

[0162] 275 kg of silica (ES747JR from Crossfield, with an average particle size of 20 μm) activated at 600° C. in nitrogen was added to the reactor in which the catalyst was prepared. Then 411 kg of 20% EADC (2.0 mmol / g silica) diluted in 555 liters of pentane was added to the reactor within 1 hour at ambient temperature. The temperature was then raised to 35°C while stirring the treated silica for one hour. ...

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Abstract

Ziegler-Natta catalyst composition capable of producing ethylene / alpha-olefins copolymers, particularly linear low density polyethylene; the composition having an improved stability of its behaviour during polymerization in respect to time. The Ziegler-Natta catalyst composition comprises: 1. Ziegler-Natta catalyst composition for the production of ethylene copolymers comprising A) a procatalyst, which procatalyst comprises a) an Al compound having the formula Al(alkyl)xCl3-x (I), where alkyl is an alkyl group with 1 to 12 and 0 = x = 3, b) a magnesium hydrocarbyloxy compound of formula Mg(OR1)2-n(R2)n (II), wherein each R1 and R2 is independently a C1-20 hydrocarbon residue which may optionally be substituted with halogen and 0 = n yTi(OR3)4-y (III), wherein R3 is a C2-20 hydrocarbon residue and y is 1, 2, 3 or 4, with compounds a), b) and c); being supported on a particulate inorganic carrier and B) a halogenated aluminium alkyl cocatalyst of the formula (IV) (C1-C4-alkyl)m-Al-X3-m, wherein X is chlorine, bromine, iodine or fluorine and m is 1 or 2.

Description

technical field [0001] The present invention relates to Ziegler-Natta catalyst compositions suitable for the preparation of ethylene polymers, especially linear low density polyethylene. [0002] More particularly, the present invention relates to Ziegler-Natta catalyst compositions capable of producing ethylene / α-olefin copolymers, especially linear low density polyethylene, and which have a time-dependent Improved performance stability. The composition comprises a mixture comprising a Group 13 metal, chlorine, magnesium and titanium atoms supported on a particulate inorganic support and an alkylaluminum halide as a cocatalyst. Background technique [0003] Typically, ethylene, alone or together with other ethylenically unsaturated monomers, is polymerized in the presence of a catalyst composition having two essential components: a transition metal compound of any group (commonly referred to as procatalyst); and a metal compound belonging to Group 1, 2 or 13 of said perio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F4/655C08F210/16
CPCC08F210/16C08F4/6555C08F210/08C08F2500/12C08F2500/18C08F2500/08C08F4/655C08F4/652C08F210/02
Inventor 托马斯·加罗夫佩伊维·瓦尔德福德尔卡勒·卡利奥维尔日尼·埃里克松
Owner BOREALIS AG
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